Chapter 11: Problem 67
How do we achieve very low temperatures with gas refrigeration cycles?
Chapter 11: Problem 67
How do we achieve very low temperatures with gas refrigeration cycles?
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Get started for freeConsider a two-stage cascade refrigeration system operating between the pressure limits of \(1.4 \mathrm{MPa}\) and \(160 \mathrm{kPa}\) with refrigerant-134a as the working fluid. Heat rejection from the lower cycle to the upper cycle takes place in an adiabatic counterflow heat exchanger where the pressure in the upper and lower cycles are 0.4 and \(0.5 \mathrm{MPa}\) respectively. In both cycles, the refrigerant is a saturated liquid at the condenser exit and a saturated vapor at the compressor inlet, and the isentropic efficiency of the compressor is 80 percent. If the mass flow rate of the refrigerant through the lower cycle is \(0.11 \mathrm{kg} / \mathrm{s}\), determine ( \(a\) ) the mass flow rate of the refrigerant through the upper cycle, \((b)\) the rate of heat removal from the refrigerated space, and ( \(c\) ) the COP of this refrigerator.
Is the efficiency of a thermoelectric generator limited by the Carnot efficiency? Why?
Why is the reversed Carnot cycle executed within the saturation dome not a realistic model for refrigeration cycles?
What are the advantages and disadvantages of absorption refrigeration?
Consider isentropic compressor of a vaporcompression refrigeration cycle. What are the isentropic efficiency and second-law efficiency of this compressor? Justify your answers. Is the second-law efficiency of a compressor necessarily equal to its isentropic efficiency? Explain.
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